US2806830A - Polyamide solutions and process of preparing same - Google Patents
Polyamide solutions and process of preparing same Download PDFInfo
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- US2806830A US2806830A US517030A US51703055A US2806830A US 2806830 A US2806830 A US 2806830A US 517030 A US517030 A US 517030A US 51703055 A US51703055 A US 51703055A US 2806830 A US2806830 A US 2806830A
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- Prior art keywords
- polyamide
- polyamides
- solution
- glutaric acid
- filaments
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- 239000004952 Polyamide Substances 0.000 title claims description 84
- 229920002647 polyamide Polymers 0.000 title claims description 84
- 238000000034 method Methods 0.000 title description 12
- 239000000203 mixture Substances 0.000 claims description 34
- JFCQEDHGNNZCLN-UHFFFAOYSA-N anhydrous glutaric acid Natural products OC(=O)CCCC(O)=O JFCQEDHGNNZCLN-UHFFFAOYSA-N 0.000 claims description 22
- RTBFRGCFXZNCOE-UHFFFAOYSA-N 1-methylsulfonylpiperidin-4-one Chemical compound CS(=O)(=O)N1CCC(=O)CC1 RTBFRGCFXZNCOE-UHFFFAOYSA-N 0.000 claims description 20
- 239000002904 solvent Substances 0.000 claims description 20
- 239000002253 acid Substances 0.000 claims description 13
- 150000007513 acids Chemical class 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 230000007062 hydrolysis Effects 0.000 claims description 7
- 238000006460 hydrolysis reaction Methods 0.000 claims description 7
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 7
- 239000011707 mineral Substances 0.000 claims description 7
- 239000000376 reactant Substances 0.000 claims description 7
- 239000012456 homogeneous solution Substances 0.000 claims description 4
- 239000000243 solution Substances 0.000 description 38
- -1 amino-acid hydrochloride Chemical class 0.000 description 10
- 239000000835 fiber Substances 0.000 description 10
- 229920000642 polymer Polymers 0.000 description 9
- 238000002166 wet spinning Methods 0.000 description 8
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- KIDHWZJUCRJVML-UHFFFAOYSA-N putrescine Chemical compound NCCCCN KIDHWZJUCRJVML-UHFFFAOYSA-N 0.000 description 6
- 150000004985 diamines Chemical class 0.000 description 5
- 150000001991 dicarboxylic acids Chemical class 0.000 description 5
- 239000012530 fluid Substances 0.000 description 5
- 239000000155 melt Substances 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 239000004014 plasticizer Substances 0.000 description 5
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 4
- TYFQFVWCELRYAO-UHFFFAOYSA-N suberic acid Chemical compound OC(=O)CCCCCCC(O)=O TYFQFVWCELRYAO-UHFFFAOYSA-N 0.000 description 4
- 229920002302 Nylon 6,6 Polymers 0.000 description 3
- 238000013019 agitation Methods 0.000 description 3
- 239000004922 lacquer Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229920002292 Nylon 6 Polymers 0.000 description 2
- 229920000305 Nylon 6,10 Polymers 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000001361 adipic acid Substances 0.000 description 2
- 235000011037 adipic acid Nutrition 0.000 description 2
- 238000010622 cold drawing Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000002074 melt spinning Methods 0.000 description 2
- 239000000123 paper Substances 0.000 description 2
- GVNWZKBFMFUVNX-UHFFFAOYSA-N Adipamide Chemical compound NC(=O)CCCCC(N)=O GVNWZKBFMFUVNX-UHFFFAOYSA-N 0.000 description 1
- 101100334009 Caenorhabditis elegans rib-2 gene Proteins 0.000 description 1
- 241000628997 Flos Species 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000003368 amide group Chemical group 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- BIVUUOPIAYRCAP-UHFFFAOYSA-N aminoazanium;chloride Chemical compound Cl.NN BIVUUOPIAYRCAP-UHFFFAOYSA-N 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 150000001896 cresols Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 238000000578 dry spinning Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000005336 safety glass Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 238000007614 solvation Methods 0.000 description 1
- 239000011877 solvent mixture Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 235000013616 tea Nutrition 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
- C08J3/09—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
- C08J3/091—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids characterised by the chemical constitution of the organic liquid
- C08J3/095—Oxygen containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2377/00—Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
Definitions
- composition of matter as defined in claim 1 wherein the solvent is glutaric acid.
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Artificial Filaments (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
compositions, and the like.
nite rates a 2,806,830 Patented Sept. 17, 1957 POLYAWE SQLUTIONS AW!) PRSCES PREPARING SAME Hohson D. De Witt, Decatur, Ala, assignor to The Chernstrand Corporation, Decatur, Ala, a corporation of Delaware NoDrawing. Application lane 21, E55,
' Serial No. 517,034
Claims. (Cl. 26-331.3
out the use of solvents, for example, by extruding the molten polyamide through a spinnezet or elongated slit to form filaments or films. However, solutions of the polyamides are likewise useful and in many applications are more advantageous than molten compositions, such as to achieve the fluid state necessary in lacquers, coating Further, solutions of the polyamides can be wet-spun into various shaped and useful articles, such as films, fibers, filaments, rods, tapes, tubes, bristles, ribbons, sheets, etc. Very often it is desirable to prepare a fluid composition for use over a period of time and in that event it is convenient if the composition can be kept in the liquid state by storage at ordinary temperatures.
In many applications it is necessary to incorporate additives in the polyamides, such as plasticizers or other modifying agents. Such addition is more advantageously accomplished by incorporating the additive in a solution of the polyamide rather than in the molten polyamide. Frequently, when such blending is done in a melt, there is a tendency toward discoloration and decomposition of the polymer. Further, there is a tendency with certain types of plasticizers and modifying agents to be less compatible at the high temperatures required for blending in a melt, whereas they can be readily incorporated in a polyamide solution at a low temperature. In addition, solutions of polyamides are more easily cast into films or coatings of uniform thickness, which is mechanically more difficult to accomplish with a molten composition due to its relatively high viscosity.
Many solvents for polyamides, as defined herein, have heretofore been proposed but most of these solvents are lacking in one or more particulars. The polyamides as a class characteristically require corrosive media as solvents, such as strong concentrated acids, phenols, cresols, and the like, particularly where solutions of the polyamides having useful degrees of concentration are required. Furthermore, and particularly when strong acids are used as solvents, degradation of the polyamide coristitutes a serious obstacle, especially at highe'r'temperatures and concentrations, and this is so even when phenolic solvents are employed.
Accordingly, it is a primary tion to overcome the aforementioned disadvantages and provide new and userul solvents for synthetic linear polyamides. It is another object of the invention to provide a new and useful composition of matter comprising a synthetic linear polyamide solution which can be formed into shaped articles, such as threads, filaments, fibers, rib- 2 bons, rods, bristles, tapes, tubes, films, and the like. It is still another object of the present invention to provide a process for preparing synthetic linear polyamide solutions in solvents which are relatively non-hazardous, noncorrosive and non-degrading. Other objects and advantages of the instant invention Will be apparent from the description thereof hereinafter.
In general, the objects of the present invention are accomplished by dissolving synthetic linear polyamides in glutaric acid or in aqueous solutions thereof containing up to 20% by weight of water. The temperature at which solution of the polyamide takes place will vary with the composition of the polyamide, its viscosity or molecular weight, whether glutaric acid or an aqueous solution thereof is employed, etc. In the case of glutaric acid alone, which is a solid at room temperature, it is neces-- sary to employ temperatures at or above the melting point (98 C.) of glutaric acid. However, when employing:
aqueous solutions of glut-aric acid, containing up to 20% water, temperatures in the range of l00 C., and.
higher, will readily effect solutions of the synthetic linearpolyamide.
The polyamides which are useful in the practice of the present invention are of the general types described in U. S. Patents 2,071,250; 2,071,253 and 2,130,948. Accordingly, throughout the instant specification and claims, the terms synthetic linear polyamides and polyamides designate the general types described in said patents.
A characteristic property of these polyamides or polymers is that they can be formed into filaments which can be cold drawn into fibers showing molecular orientation along the fiber axis. The polyamides are particularly useful for the preparation of fibers, bristles, sheets, rods, tubes, and the like. The polyamides are of two types, those obtainable from polymerizable monoaminomonocarboxylic acids and their amide-forming derivatives, for example, caprolactam, and those obtainable from the reaction of suitable diarnines and suitable dicarboxylic acids or amide-forming derivatives of dibasic carboxylic acids. in these polyamides the amide group forms an integral part of the main chain of atoms in the polymer. On hydrolysis with strong mineral acids, the polyamides revert to monomeric polyamide-forming reactants. In accordance with the present invention, solutions or dopes containing'from 5 to 25% by weight of polyamide are suitable for the formation of filaments and fibers. The concentration of the polyamides which can be obtained in solution and the viscosity of the solution depend upon the nature of the polymer, the solvent employed and the temperature. Usually, when making a solution of a polyamide which is to be employed inthe manufacture of fibers and filaments, a polyamide having an intrinsic viscosity of to 2.0 or above is employed. For example, as much as 20-25% by Weight of the polyhexamethylene adipamide having an intrinsic viscosity of about 0.36 can be dissolved in glutaric acid at 98 C. Polyarnides having a lower molecular weight or intrinsic viscosity are employed when the solution or dope is to be used for coating or as a lacquer. \Vhile it is preferred to employ 5 to 25% by weight of the polyamide in the solution when the solution is to be used in forming fibers and filaments, it is to be understood that less than 5% or more than 25% polyamide may be used when the solution is to be employed forother purposes, such as coating, or in lacquers, and the like, or when low molecular weight polyamides are employed. The amount of any specific polyamide, which can be dissolved in the solvent or solvent mixtures of the present invention, will be readily evident to those skilled in the art.
Generally, heating of the solutions is accomplished on a water or oil bath. However, other means may be en;-
.diamine hydrochloride.
3. ployed, if desired. Agitation of the mixture during the heating process is preferred but it should be understood that agitation is not always necessary nor critical. Agitation can be accomplished by any suitable means, such as by stirring, shaking, etc.
While each polymer Varies somewhat'in its solubility characteristics and the temperature of solvation, this invention is applicable to all synthetic linear polyamides, as hereinbefore defined. As indicated, the polyamides are generally of two types, those derived from polymerizable monoaminomonocarboxylic acids or their amide-forming derivatives, and those derived from the reaction of suitable diamines with suitable dicarboxylic acids or amide forming derivatives of dicarboxylic acids. On hydrolysis with mineral acids, the polyamides yield monomeric polyamide-forming reactants. For example, a polyamide derived from a diamine and a dibasic acid yields on bydrolysis with hydrochloric acid, the dibasic acid and the Similarly, an amino-acid type polyamide yields an amino-acid hydrochloride. Particularly useful polyamides in the present invention are the simple unsubstituted polyamides, such as those formed by the reaction of tetramethylene diamine with adipic acid, tetramethylene diamine with suberic acid, tetramethylene diamine with sebacic acid, hexarnethylene diamine with adipic acid, hexamethylene diamine with suberic acid,
' hexamethylene diamine with sebacic acid, the polymerization products of epsilon-caprolactam, etc. In addition, polymers formed from the reaction of two or more diamines with dicarboxylic acids and/or two or more dicarboxylic acids with diamines are contemplated in the practice of the instant invention. These polymers all dissolve in glutaric acid and aqueous solutions thereof, as hereinbefore defined, in accordance with the present invention as do the inter-polymers which are normally insoluble in most simple alcohols.
The most useful polyamides are the high molecular weight polyamides, that is, those having an intrinsic viscosity of 0.3 or above, since they possess the property of being formed into filaments which can be cold-drawn. That is, filaments produced from the present polyamide compositions have the ability to accept a very high degree of permanent orientation under stress. By the application of moderate stress at ordinary temperatures these filaments can be instantly elongated or cold-drawn. The filaments can be cold-drawn as much as several times their original lengths. The cold-drawing operations may be carried out on filaments, which have been allowed to cool fully and solidify, or the cold-drawing may follow the formation of the filaments directly as one part of a continuous process. The filaments, which are cold-drawn, possess a high degree of permanent orientation along the filaments axis, as shown by characteristic X-ray patterns. These high molecular weight varieties of the polyamides are more useful for most purposes than the lower molecular weight polyamides since they excel in toughness and durability.
The polyamide compositions of the instant invention are particularly useful for. the formation of shaped articles by the so-called Wet-spinning technique wherein a solution or dope of the polyamide is extruded through a suitably shaped orifice into a bath comprising a non-solvent for the polyamide. It is particularly desirable to employ the wet-spinning technique,-if at all possible, and the present invention provides the means of wet-spinning polyamide structures. The wet-spinning method has a number of advantages over the melt-spinning technique, which is presently widely used, for example, the wet-spinning method is generally more economical and can be operated at lower temperatures than melt-spinning. Because of the lower temperatures, plasticizers and other modifying agents can be more advantageously added to a solution rather than to a' molten polyamide, thereby minimizing the tendency toward discolorationand decom- 7 position. Further. there is a tendency with certain types of plasticizers and modifying agents to be less compatible at the high temperatures required for blending in a melt, whereas they can be readily incorporated in a polyamide solution at a low temperature. A still further advantage in the use of solutions lies in the ease with which they can e cast into films or coatings of uniform thickness, which is mechanically more difficult to accomplish with a molten composition due to its relatively high viscosity.
While the wet-spinning technique for forming shaped articles from polyamides is preferred, as pointed out above, it has not been employed commercially due to the scarcity of suitable solvents, since polyamides are generally insoluble in most of the well known organic solvents. Therefore, the present invention is advantageous in that it answers a serious need which has existed for the discovery of a suitable solvent for the Wet-spinning of polyamide shaped articles and one which provides polyamide solutions of suitable concentration and stability which can be prepared conveniently with standard equipment. In addition, the solvent of the present invention can readily and conveniently be recovered for reuse or re-cycling during the employment of the polyamide solutions for transforming the polyamide into other forms, such as filaments, fibers, films, and the like.
For a more detailed description of the present invention, reference is bad to the following specific examples which are merely intended to be illustrative and not limitative, In the examples, all parts and percent are by weight unless otherwise indicated.
Example I 7 Two parts of glutaric acid were placed in a tube and heated to a temperature of 98 C. To the melt obtained there was added 0.25 part of polyhexamethylene adip-' Ten parts of glutaric acid and 1 part of water were warmed together in a tube and the solution obtained was heated to 100 C. 1.5 parts of polyhexamethylene adipamide were added to the hot solution. The polyamide dissolved rapidly yielding a clear, homogeneous and fluid solution. Filaments were obtained upon extrusion of the polyamide solution into methanol.
Example HI Two parts of glutaric acid were heated in a tube to 100 C. To the melt obtained there was added 0.25 part of polycaprolactam. The polyamide dissolved rapidly and gave a clear, fluid solution. Addition of 0.2 part of water caused no precipitation and gave a more fluid solu tion. Polyarnide filaments were formed by extrusion of the solution into water and also into methanol.
In addition to use in wet-spinning, the polyamide solutions or compositions of this invention may be employed in dry-spinning wherein the solution or dope is extruded through a suitably shaped orifice into a heated atmosphere capable of evaporating the solvent from the newly formed article.
The properties of the objects formed from the polyamide compositions herein described may be modified by appropriate modification of the compositions. Thus, the compositions of this invention may have incorporated therein various modifying agents, such as plasticizers, dyes, pi ments, diluents, resins, cellulose derivatives. waxes, water repellants, luster modifying agents, flame repellents, and the like. Solutions of difierent polyamides, or of polyamides with other polymers or solutes can be solution blended and precipitated .to give homogeneous blends, where melt blending is undesirable or impractical.
In addition to the formation of filaments, fibers, films, etc., the instant polyamide compositions can be formed into a variety of other objects, for example, bristles, surgical sutures, fishing leaders, fishline, dental floss, ribbons, sheets, safety glass inner layers, golf ball covers, and plasticized or otherwise modified solid compositions useful for making molded articles. The instant polyamide compositions are also useful for coating wire, fabrics, paper, regenerated cellulose, and the like, and for impregnating fabric, paper, and other porous materials. Numerous other advantages of the instant invention will be apparent to those skilled in the art.
As many apparently widely different embodiments of this invention may be made without departing from the spirit and scope thereof, it is to be understood that the invention is not limited to the specific embodiments thereof except as defined in the appended claims.
I claim:
1. As a new composition of matter, a clear homogeneous solution comprising a synthetic linear polyamide, which upon hydrolysis with strong mineral acids yields monomeric polyamide-forming reactants, dissolved in a solvent selected from the group consisting of glutaric acid and mixtures of glutaric acid with not more than 20 percent by weight of water.
2. A composition of matter as defined in claim 1 wherein the polyamide is polycaprolactam.
'3. A composition of matter as defined in claim 1 wherein the polyamide is polyhexamethylene adiparnide.
4. A composition of matter as defined in claim 1 wherein the polyamide is polyhexamethylene sebacamide.
5. A composition of matter as defined in claim 1 wherein the polyamide is polytetramethylene adipamide.
6. A composition of matter as defined in claim 1 wherein the polyamide is polytetramethylene sebacamide.
7. A composition of matter as defined in claim 1 wherein the solvent is glutaric acid.
8. A process for preparing a new composition of matter comprising mixing a synthetic linear polyamide, which upon hydrolysis with strong mineral acids yields monomeric polyamide-forming reactants, with a solvent selected from the group consisting of glutaric acid and mixtures of glutaric acid with not more than 20 percent by weight of water, and heating said mixture to a temperature of at teas; 90 C. to form a clear homogeneous solution.
The process as defined in claim 8 wherein the polya'ni' e is po-lycaprolactam.
The process as defined in claim 8 wherein the polyamide is polyhexamethylene adipamide.
ii. The process as defined in claim 8 wherein the polyamide is polyhexamethylene sebacamide.
12. The process as defined in claim 8 wherein the polyamide is polytetramethylene adiparnide.
13. The process as defined in claim 8 wherein the polyamide is polytetramethylene sebacamide.
I 14. A process for preparing a new fiber-forming composition of matter comprising heating glutaric acid to a temperature of at least 98 C. and thereafter adding suificient synthetic linear polyamide having an intrinsic viscosity in the range of 0.3 to 2.0 to the hot glutaric acid to form a clear homogeneous solution containing from 5 to 25 percent by weight of the polyamide, based on the weight of the solution, said polyamide being one which upon hydrolysis with strong mineral acids yields monomeric polyamide-forming reactants.
15. As a new composition of matter, a clear homogeneous fiber-forming solution comprising a synthetic linear polyamide, which upon hydrolysis with strong mineral acids yields monomeric polyamide-forming reactants, having an intrinsic viscosity from 0.3 to 2.0, dissolved in a solvent selected from the group consisting of glutaric acid and mixtures of glutaric acid with not more than 20 percent by weight of water.
References Cited in the file of this patent UNITED STATES PATENTS 2,265,119 Coolidge Dec. 2, 1941
Claims (1)
1. AS A NEW COMPOSITION OF MATTER, A CLEAR HOMOGENEOUS SOLUTION COMPRISING A SYNTHETIC LINEAR POLYAMIDE, WHICH UPON HYDROLYSIS WITH STRONG MINERAL ACIDS YIELDS MONOMERIC POLYAMIDE-FORMING REACTANTS, DISSOLVED IN A SOLVENT SELECTED FROM THE GROUP CONSISTING OF GLUTARIC ACID AND MIXTURES OF GLUTARIC ACID WITH NOT MORE THAN 20 PERCENT BY WEIGHT OF WATER.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US517030A US2806830A (en) | 1955-06-21 | 1955-06-21 | Polyamide solutions and process of preparing same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US517030A US2806830A (en) | 1955-06-21 | 1955-06-21 | Polyamide solutions and process of preparing same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2806830A true US2806830A (en) | 1957-09-17 |
Family
ID=24058097
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US517030A Expired - Lifetime US2806830A (en) | 1955-06-21 | 1955-06-21 | Polyamide solutions and process of preparing same |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2806830A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3003983A (en) * | 1958-09-25 | 1961-10-10 | Chemstrand Corp | Polyamides and polyurethanes dissolved in a mixture of water and phytic acid and process of making same |
| US3179618A (en) * | 1960-06-27 | 1965-04-20 | Celanese Corp | Shaped condensation polymers |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2265119A (en) * | 1939-06-12 | 1941-12-02 | Du Pont | Polyamide |
-
1955
- 1955-06-21 US US517030A patent/US2806830A/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2265119A (en) * | 1939-06-12 | 1941-12-02 | Du Pont | Polyamide |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3003983A (en) * | 1958-09-25 | 1961-10-10 | Chemstrand Corp | Polyamides and polyurethanes dissolved in a mixture of water and phytic acid and process of making same |
| US3179618A (en) * | 1960-06-27 | 1965-04-20 | Celanese Corp | Shaped condensation polymers |
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